Encyclopedia of Renewable Energy. James G. Speight

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cooking oil is a valuable asset for conversion to liquid fuels, and the quantity of biodiesel which could be produced from waste cooking oil can be quantified in a manner similar to that of biodiesel produced direct from agriculture. The only difference is that rather than calculating crop yields, it is necessary to quantify the amount of waste oil available.

      Biodiesel is a light to dark yellow liquid that is immiscible with water and has a high boiling point, low vapor pressure, a flash point of approximately 150°C (300°F), and a density on the order of 0.88 g/cm³. Biodiesel has a viscosity similar to petrodiesel (the current term to differentiate the different forms of diesel) and can be used as an additive in formulations of diesel to increase the lubricity of pure ultra-low sulfur diesel (ULSD) fuel.

      Almost any variety of oil or grease (from new food-grade vegetable oil to used cooking oil or trap grease to wastewater treatment-plant grease) can be converted into biodiesel. However, the amounts of reactants (oil, methanol, and sodium hydroxide) vary to some degree, depending on what oil is used. The amount of methanol and sodium hydroxide must be sufficient to react with the vegetable oil, but excessive amounts of these reactants should not be used. Just as an engine requires excess air to be sure that all the fuel burns, it takes excess methanol to be sure all of the oil reacts.

      The chemistry of biodiesel production is known as transesterification insofar as the process involves reaction of glycoside-containing plant oil with a short chain alcohol such as methanol or ethanol. The feedstocks are typically animal, and plant fats and oils are typically made of triglycerides which are esters of free fatty acids with the trihydric alcohol, glycerol. In the transesterification reaction, the alcohol is deprotonated with a base to make it a stronger nucleophile. Commonly, ethanol or methanol is used. Usually, the reaction proceeds at a low rate; heat, as well as an acid or base, is used to help the reaction proceed more quickly.

      Almost all biodiesel from waste oil is produced using the base-catalyzed technique as it is the most economical process, requiring only low temperatures and pressures and producing over 98% conversion yield (provided the starting oil is low in moisture and free fatty acids). The major steps required to synthesize biodiesel are purification, neutralization, and transesterification.

      Purification: the waste vegetable oil is filtered to remove dirt, charred food, and other non-oil material often found. Water is removed because its presence causes the triglycerides to hydrolyze to give salts of the fatty acids instead of undergoing transesterification to give biodiesel. The crude oil may be stirred with a drying agent such as magnesium sulfate to remove the water in the form of water of crystallization. The drying agent can be separated by decanting or by filtration, but the viscosity of the oil may not allow the drying agent to mix thoroughly.

      Neutralization of free fatty acids: A sample of the cleaned oil is titrated against a standard solution of base in order to determine the concentration of free fatty acids (RCOOH) present in the waste vegetable oil sample. The quantity of base required to neutralize the acid is then calculated.

      Transesterification: While adding the base, a slight excess is factored in to provide the catalyst for the transesterification. The calculated quantity of base (usually sodium hydroxide) is added slowly to the alcohol, and it is stirred until it dissolves. Sufficient alcohol is added to make up three full equivalents of the triglyceride, and an excess is added to drive the reaction to completion. The solution of sodium hydroxide in the alcohol is then added to a warm solution of the waste oil, and the mixture is heated (typically 50°C, 122°F) for several hours (4 to 8 typically) to allow the transesterification to proceed. A condenser may be used to prevent the evaporative losses of the alcohol. Care must be taken not to create a closed system which can explode.

      Workup: Once the reaction is complete, the glycerol should sink. When ethanol is used, it is reported that an emulsion often forms. This emulsion can be broken by standing, centrifugation, or the addition of a low boiling (easily removed) non-polar solvent, decanting, and distilling. The top layer, a mixture of biodiesel and alcohol, is decanted. The excess alcohol can be distilled off, or it can be extracted with water. If the latter is used, the biodiesel should be dried by distillation or with a drying agent.

      Biodiesel – Production and Properties

      Biodiesel is a diesel-equivalent fuel derived from biological sources (such as vegetable oil) which can be used in unmodified diesel-engine vehicles. It is thus distinguished from the straight vegetable oil or waste vegetable oil used as fuels in some diesel vehicles.

Schematic illustration of biodiesel Production Path.

      Biodiesel is made through a chemical process (transesterification) whereby the glycerin is separated from the fat or vegetable oil. The process leaves behind two products: (i) methyl esters and (ii) glycerin (a valuable by-product usually sold to be used in soaps and other products).

      The primary products of transesterification are methyl esters (biodiesel) and glycerol. 100 lbs of soybean oil are reacted with 10 lbs of methanol and 1 lbs of catalyst yielding 100 lbs of biodiesel and 10 lbs of glycerol. Glycerol is decanted and removed first as it is heavier and sinks. Methanol is recycled in the process by washing both the glycerol and biodiesel with water to remove unreacted methanol and return it to the process. Glycerol, a valuable by-product, is approximately 88% pure and can be further processed to pharmaceutical grade glycerol.

Property Source: waste cooking oil Source: animal tallow Commercial diesel fuel
Density (kg/l at 15oC) 0.890 -0.897 0.856 - 0.877 0.075-0.840
Flash point (oC) 196 30 to 35 67 to 85
Pour point (oC) 11

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